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JPH0697101B2 - Heating system - Google Patents
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JPH0697101B2 - Heating system - Google Patents

Heating system

Info

Publication number
JPH0697101B2
JPH0697101B2 JP21655388A JP21655388A JPH0697101B2 JP H0697101 B2 JPH0697101 B2 JP H0697101B2 JP 21655388 A JP21655388 A JP 21655388A JP 21655388 A JP21655388 A JP 21655388A JP H0697101 B2 JPH0697101 B2 JP H0697101B2
Authority
JP
Japan
Prior art keywords
liquid
refrigerant
gas
receiver
liquid separator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP21655388A
Other languages
Japanese (ja)
Other versions
JPH0264326A (en
Inventor
達規 桜武
克彦 山本
勝蔵 粉川
純一 雀堂
紘一郎 山口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP21655388A priority Critical patent/JPH0697101B2/en
Publication of JPH0264326A publication Critical patent/JPH0264326A/en
Publication of JPH0697101B2 publication Critical patent/JPH0697101B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Central Heating Systems (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は冷媒を加熱し無動力熱搬送方式で暖房運転する
暖房装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating device that heats a refrigerant and performs heating operation by a non-powered heat transfer system.

従来の技術 従来のこの種の暖房装置は第3図に示すように冷媒加熱
器1より上方に位置した受液器2の中間位置に気液分離
器3を配設し前記受液器2と前記気液分離器3の間に両
者を均圧させる開閉弁4を有しさらに受液器2と気液分
離器3の間に逆止弁5を設け、冷媒加熱器1で蒸発した
冷媒は放熱器6で凝縮し受液器2へ流入する。受液器2
へ液冷媒が溜ると開閉弁4を開き受液器2と気液分離器
3とを均圧化し受液器2の液冷媒を気液分離器3へ流入
させる。流入し終わると開閉弁4を閉じ逆止弁5も閉じ
るため再び放熱器6から凝縮した液冷媒が受液器2へ流
入する。このような動作を繰り返して熱搬送を行い暖房
運転を行うようになっていた(例えば実開昭61-43679号
公報) 発明が解決しようとする課題 しかしながら上記従来の構成では、冷媒加熱器での加熱
量に必要な冷媒循環量Gは次式で表わされる。
2. Description of the Related Art In a conventional heating device of this type, as shown in FIG. 3, a gas-liquid separator 3 is arranged at an intermediate position of a liquid receiver 2 located above a refrigerant heater 1 and the liquid receiver 2 is provided. An on-off valve 4 for equalizing the pressure of the two is provided between the gas-liquid separator 3, and a check valve 5 is further provided between the liquid receiver 2 and the gas-liquid separator 3, so that the refrigerant evaporated in the refrigerant heater 1 The heat is condensed by the radiator 6 and flows into the liquid receiver 2. Receiver 2
When the liquid refrigerant accumulates, the on-off valve 4 is opened to equalize the pressure between the liquid receiver 2 and the gas-liquid separator 3 and allow the liquid refrigerant in the liquid receiver 2 to flow into the gas-liquid separator 3. When the inflow is completed, the on-off valve 4 is closed and the check valve 5 is also closed, so that the liquid refrigerant condensed from the radiator 6 again flows into the liquid receiver 2. The above-described operation is repeated to perform heat transfer to perform heating operation (for example, Japanese Utility Model Laid-Open No. 61-43679). Problems to be Solved by the Invention However, in the above conventional configuration, the refrigerant heater is used. The refrigerant circulation amount G required for the heating amount is expressed by the following equation.

G=V×γ/T G:加熱量に必要な冷媒循環量(g/sec) V:受液器容積(cc) γ:受液器内液冷媒密度(g/cc) T:開閉弁の周期(開時間プラス閉時間)(sec) この式から明らかなように開閉弁の周期が同じでもその
開時間と閉時間の設定の仕方により、暖房サイクルの圧
力が異なり暖房運転時室内温度が上昇するとその圧力が
異常上昇し、その結果暖房運転範囲が狭くなり、それを
防止するために放熱器が大きくなるという課題を有して
いた。
G = V × γ / TG: Refrigerant circulation amount required for heating amount (g / sec) V: Liquid receiver volume (cc) γ: Liquid refrigerant density in receiver (g / cc) T: Open / close valve cycle (Opening time + Closing time) (sec) As is clear from this equation, even if the on-off valve cycle is the same, the heating cycle pressure will differ depending on how the opening time and closing time are set. There is a problem that the pressure rises abnormally, the heating operation range is narrowed as a result, and the radiator becomes large in order to prevent it.

本発明は上記従来の課題を解消するもので放熱器を大き
くすることなく暖房サイクルの圧力の異常上昇を防止し
暖房運転範囲の拡大を目的とするものである。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems, and an object of the present invention is to prevent an abnormal increase in the pressure of the heating cycle and to expand the heating operation range without increasing the size of the radiator.

課題を解決するための手段 上記目的を達成するために本発明の暖房装置は、冷媒加
熱器を気液分離器より下方に配設し前記冷媒加熱器と前
記気液分離器とを冷媒加熱器入口管と冷媒加熱器出口管
とでループ状に接続配管する一方、受液器を前記気液分
離器より上方に配設し放熱器、第1逆止弁、前記受液
器、第2逆止弁、前記気液分離器を接続配管すると共に
前記受液器と前記冷媒加熱器出口管との間に開閉弁を有
する均圧管を設け、前記開閉動作周期の開時間を閉時間
より短く設定した制御装置を備えたものである。
Means for Solving the Problems In order to achieve the above object, the heating device of the present invention is arranged such that a refrigerant heater is disposed below a gas-liquid separator, and the refrigerant heater and the gas-liquid separator are the refrigerant heater. The inlet pipe and the refrigerant heater outlet pipe are connected to form a loop, while the liquid receiver is disposed above the gas-liquid separator and the radiator, the first check valve, the liquid receiver, and the second reverse A stop valve and a gas-liquid separator are connected, and a pressure equalizing pipe having an opening / closing valve is provided between the liquid receiver and the refrigerant heater outlet pipe, and the opening time of the opening / closing operation cycle is set shorter than the closing time. It is equipped with a control device.

作用 本発明は上記した構成により、第2図の開閉弁閉時間中
の受液器減圧特性(放熱器から出た液冷媒温度すなわち
受液器入口側液冷媒温度が低くて冷媒加熱器蒸発温度が
高い程受液器内減圧量が大きい事を示すもの)からいま
開時間が閉時間より長い場合(第2図にAモードで示
す)その閉時間内へ開時間中気液分離器から放熱器へ出
ていく冷媒量を受液器へ溜めなければならないため、閉
時間中の受液器減圧量を大きくとらなければならず、実
際の暖房運転では室温以下には液冷媒温度は低くならな
いため蒸発温度が上昇しサイクル圧力が上昇するのに対
し開閉弁の開時間が閉時間より短い場合(第2図にBモ
ードで示す)は閉時間が長いため閉時間中の受液器減圧
量はAモードに比べ小さくてよく蒸発温度(サイクル圧
力)は低くなるように作用する。
Action The present invention has the above-described configuration, and the receiver decompression characteristic during the on-off valve closing time of FIG. 2 (the liquid refrigerant temperature from the radiator, that is, the liquid refrigerant temperature at the receiver inlet side is low and the refrigerant heater evaporation temperature is Indicates that the higher the pressure is, the larger the decompression amount in the receiver is). If the opening time is now longer than the closing time (shown as A mode in Fig. 2), the heat is released from the gas-liquid separator during the opening time to the closing time. Because the amount of refrigerant flowing out to the receiver must be stored in the receiver, the receiver pressure reduction amount during the closing time must be large, and in actual heating operation the liquid refrigerant temperature will not drop below room temperature. Therefore, when the opening temperature of the on-off valve is shorter than the closing time (shown in B mode in Fig. 2) while the evaporation temperature rises and the cycle pressure rises, the closing time is long and the decompression amount of the receiver during the closing time is large. Is smaller than A mode, and evaporation temperature (cycle pressure) is low. Acts like.

実施例 以下本発明の一実施例を第1図にもとづいて説明する。
なお第2図と同一部材には同一番号を付している。
Embodiment One embodiment of the present invention will be described below with reference to FIG.
The same members as those in FIG. 2 are designated by the same reference numerals.

第1図において1は冷媒加熱器であって、気液分離器3
より下方に配設している。そして気液分離器3と冷媒加
熱器入口管7と、冷媒加熱器出口管8とでループ状に接
続されている。2は受液器であり気液分離器3より上方
に設けられ、第2逆止弁5を介して気液分離器3に連通
されている。6は放熱器、9は第1逆止弁である。そし
て、冷媒加熱器1、冷媒加熱器出口管8、気液分離器
3、及び冷媒加熱器入口管7とで構成する自然循環回路
と、気液分離器3、放熱器6、第1逆止弁9、受液器2
及び第2逆止弁5とで構成する冷媒循環回路を有してい
る。
In FIG. 1, 1 is a refrigerant heater, which is a gas-liquid separator 3
It is arranged below. The gas-liquid separator 3, the refrigerant heater inlet pipe 7 and the refrigerant heater outlet pipe 8 are connected in a loop. A liquid receiver 2 is provided above the gas-liquid separator 3 and is connected to the gas-liquid separator 3 via a second check valve 5. Reference numeral 6 is a radiator, and 9 is a first check valve. Then, the natural circulation circuit constituted by the refrigerant heater 1, the refrigerant heater outlet pipe 8, the gas-liquid separator 3, and the refrigerant heater inlet pipe 7, the gas-liquid separator 3, the radiator 6, and the first check valve. Valve 9, receiver 2
And a second check valve 5 and a refrigerant circulation circuit.

更に前記受液器2と前記冷媒加熱器出口管8の間に開閉
弁4を有する均圧管10を配設してある。また11は前記開
閉弁の開閉時間を制御する制御装置である。
Further, a pressure equalizing pipe 10 having an opening / closing valve 4 is arranged between the liquid receiver 2 and the refrigerant heater outlet pipe 8. Further, 11 is a control device for controlling the opening / closing time of the opening / closing valve.

上記構成において冷媒加熱器1で加熱された冷媒は、二
相状態で冷媒加熱器出口管8を通り気液分離器3内に流
入し液冷媒は再び冷媒加熱器入口管7を通って冷媒加熱
器1へ流入する。一方気液分離器3内に冷媒加熱器1か
ら流入した二相冷媒のガス冷媒は放熱器6で凝縮液化す
る。この時開閉弁4が閉の時は第2逆止弁は閉状態で受
液器2へ放熱器6からの凝縮液冷媒が第1逆止弁9を通
り圧送され少し液冷媒が流入すると受液器2内の圧力は
減圧されて放熱器6から凝縮液で満たされる。次に開閉
弁4を開にすると受液器2と気液分離器3とは均圧状態
となり受液器2内の液冷媒は第2逆止弁5を通り気液分
離器3内へ流入する。この時第1逆止弁9は閉状態であ
る。次に開閉弁4を閉とすると第2逆止弁5は閉となり
再び受液器2へ放熱器6から凝縮液冷媒が流入し次に開
閉弁4を開にするというサイクルを繰返す。すなわち気
液分離器3と冷媒加熱器1の間は自然循環サイクル、気
液分離器3、放熱器6、第1逆止弁9、受液器2、及び
第2逆止弁5とで構成される冷媒循環回路は、受液器2
へ放熱器6から流入してくる液冷媒を溜めてそれを間欠
的に気液分離器3へ供給するという間欠動作サイクルで
ある。ここで制御装置11により開閉弁4の開時間を閉時
間より短く設定しているので開時間中気液分離器3から
放熱器6へ流出した冷媒量を閉時間中に受液器3へ引き
戻す際受液器3内の減圧量は少なくてよく放熱器6の凝
縮温度に対する放熱器出口液冷媒過冷却度は小さくてよ
いので暖房サイクルの圧力上昇を防止でき放熱器の大き
さを大きくすることなく暖房運転範囲の拡大が図れる。
In the above configuration, the refrigerant heated by the refrigerant heater 1 flows into the gas-liquid separator 3 through the refrigerant heater outlet pipe 8 in a two-phase state, and the liquid refrigerant again passes through the refrigerant heater inlet pipe 7 to heat the refrigerant. Flows into vessel 1. On the other hand, the gas refrigerant of the two-phase refrigerant flowing into the gas-liquid separator 3 from the refrigerant heater 1 is condensed and liquefied by the radiator 6. At this time, when the on-off valve 4 is closed, the second check valve is closed, and the condensed liquid refrigerant from the radiator 6 is pumped to the liquid receiver 2 through the first check valve 9 and a small amount of liquid refrigerant flows into the receiver 2. The pressure in the liquid container 2 is reduced and the radiator 6 is filled with the condensate. Next, when the opening / closing valve 4 is opened, the liquid receiver 2 and the gas-liquid separator 3 are in a pressure equalizing state, and the liquid refrigerant in the liquid receiver 2 flows into the gas-liquid separator 3 through the second check valve 5. To do. At this time, the first check valve 9 is closed. Next, when the opening / closing valve 4 is closed, the second check valve 5 is closed, the condensed liquid refrigerant flows into the liquid receiver 2 from the radiator 6 again, and then the opening / closing valve 4 is opened. That is, a natural circulation cycle, a gas-liquid separator 3, a radiator 6, a first check valve 9, a liquid receiver 2 and a second check valve 5 are provided between the gas-liquid separator 3 and the refrigerant heater 1. The refrigerant circulation circuit used is the receiver 2
This is an intermittent operation cycle in which the liquid refrigerant flowing from the radiator 6 is collected and is intermittently supplied to the gas-liquid separator 3. Here, since the opening time of the on-off valve 4 is set shorter than the closing time by the control device 11, the amount of the refrigerant flowing out from the gas-liquid separator 3 to the radiator 6 during the opening time is returned to the liquid receiver 3 during the closing time. At this time, the amount of decompression in the liquid receiver 3 may be small and the radiator outlet liquid refrigerant subcooling degree with respect to the condensation temperature of the radiator 6 may be small, so that the pressure rise in the heating cycle can be prevented and the size of the radiator can be increased. Therefore, the heating operation range can be expanded.

発明の効果 以上のように本発明の暖房装置によれば、開閉弁の開時
間を閉時間より短く設定しているため、放熱器凝縮温度
に対する放熱器出口液冷媒過冷却度を小さくする事がで
き(受液器の減圧量を小さくし、閉時間を長くする事に
より受液器へ必要液冷媒を戻してやる)暖房サイクルの
圧力上昇を防止でき、放熱器の大きさを大きくすること
なく暖房運転範囲の拡大が図れる。さらに受液器内減圧
量を小さくできるため開閉弁閉時受液器内へ凝縮液冷媒
が流入する流動音の防止にも効果がある。
As described above, according to the heating device of the present invention, since the opening time of the on-off valve is set shorter than the closing time, it is possible to reduce the radiator outlet liquid refrigerant supercooling degree with respect to the radiator condensation temperature. Yes (by reducing the decompression amount of the receiver and returning the necessary liquid refrigerant to the receiver by increasing the closing time) It is possible to prevent pressure increase in the heating cycle and to heat without increasing the size of the radiator. The operating range can be expanded. Furthermore, since the amount of decompression in the receiver can be reduced, it is also effective in preventing the flow noise of the condensed refrigerant flowing into the receiver when the on-off valve is closed.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の一実施例による暖房装置の回路構成
図、第2図は受液器減圧量変化特性図、第3図は従来の
暖房装置の回路構成図である。 1……冷媒加熱器、2……受液器、3……気液分離器、
4……開閉弁、5……第2逆止弁、6……放熱器、9…
…第1逆止弁、11……制御装置。
FIG. 1 is a circuit configuration diagram of a heating device according to an embodiment of the present invention, FIG. 2 is a characteristic diagram of change in liquid receiver pressure reduction amount, and FIG. 3 is a circuit configuration diagram of a conventional heating device. 1 ... Refrigerant heater, 2 ... Liquid receiver, 3 ... Gas-liquid separator,
4 ... on-off valve, 5 ... second check valve, 6 ... radiator, 9 ...
… First check valve, 11 …… Control device.

フロントページの続き (72)発明者 雀堂 純一 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 山口 紘一郎 大阪府門真市大字門真1006番地 松下電器 産業株式会社内Front page continuation (72) Inventor Junichi Jundo, Kadoma City, Osaka Prefecture 1006 Kadoma, Matsushita Electric Industrial Co., Ltd. (72) Koichiro Yamaguchi, Kadoma City, Osaka Prefecture 1006 Kadoma, Matsushita Electric Industrial Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】冷媒加熱器を気液分離器より下方に配設
し、前記冷媒加熱器と前記気液分離器とを冷媒加熱器入
口管と冷媒加熱器出口管とで連通する一方、受液器を前
記気液分離器より上方に配設して放熱器、第1逆止弁、
前記受液器、第2逆止弁、及び前記気液分離器をループ
状に連通すると共に前記受液器と前記冷媒加熱器出口管
との間に開閉弁を有する均圧管を設け、前記開閉弁の開
時間を閉時間より短く設定した制御装置から成る暖房装
置。
1. A refrigerant heater is disposed below a gas-liquid separator, and the refrigerant heater and the gas-liquid separator are communicated with each other by a refrigerant heater inlet pipe and a refrigerant heater outlet pipe. The liquid container is disposed above the gas-liquid separator, and the radiator, the first check valve,
The liquid receiver, the second check valve, and the gas-liquid separator are connected in a loop, and a pressure equalizing pipe having an opening / closing valve is provided between the liquid receiver and the refrigerant heater outlet pipe. A heating system consisting of a control unit that sets the opening time of the valve shorter than the closing time.
JP21655388A 1988-08-31 1988-08-31 Heating system Expired - Fee Related JPH0697101B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21655388A JPH0697101B2 (en) 1988-08-31 1988-08-31 Heating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21655388A JPH0697101B2 (en) 1988-08-31 1988-08-31 Heating system

Publications (2)

Publication Number Publication Date
JPH0264326A JPH0264326A (en) 1990-03-05
JPH0697101B2 true JPH0697101B2 (en) 1994-11-30

Family

ID=16690239

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21655388A Expired - Fee Related JPH0697101B2 (en) 1988-08-31 1988-08-31 Heating system

Country Status (1)

Country Link
JP (1) JPH0697101B2 (en)

Also Published As

Publication number Publication date
JPH0264326A (en) 1990-03-05

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